EP2480335B1 - Zyklon zur abscheidung klebriger partikel aus gasströmen - Google Patents
Zyklon zur abscheidung klebriger partikel aus gasströmen Download PDFInfo
- Publication number
- EP2480335B1 EP2480335B1 EP10744879.7A EP10744879A EP2480335B1 EP 2480335 B1 EP2480335 B1 EP 2480335B1 EP 10744879 A EP10744879 A EP 10744879A EP 2480335 B1 EP2480335 B1 EP 2480335B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cyclone
- gas streams
- particles
- sticky particles
- separating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000002245 particle Substances 0.000 title claims description 41
- 239000011248 coating agent Substances 0.000 claims description 4
- 238000000576 coating method Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 27
- 238000007654 immersion Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 238000005411 Van der Waals force Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/16—Auxiliary treatment of granules
Definitions
- This invention relates to a cyclone for separating sticky particles from gas streams and to a use of the cyclone.
- Centrifugal separators in the form of cyclones are known.
- gas cleaning for example, they serve for separating solid particles contained in the gases.
- the gases are put into a rotary movement due to their own flow velocity and the corresponding constructive design of the cyclone.
- the centrifugal forces acting on the particles accelerate the same radially to the outside. They are thereby separated from the gas stream which is passed to the inside and discharged.
- the gases to be cleaned contain sticky particles, however, it is disadvantageous when accretions of particles occur inside the cyclone, which leads to a deterioration of the separation efficiency of the cyclone.
- the gas cleaning in the cyclone must then be interrupted with great effort and the cyclone must be liberated from the accretions, so that the separation efficiency of the cyclone can again be increased.
- Document EP 0 346 748 A2 discloses a cyclone separator suitable for separating particles from a gas stream wherein the housing of the cyclone is closed by a planar cover lying in the radial plane of the cyclone housing.
- the gas stream is introduced via an inlet duct extending along a spiral arch that tangentially joins with the wall of the cyclone housing.
- the inlet duct extends with its radial outer end vertically above the cover and is inclined with a concave structure towards the inner end of the spiral arch.
- the lower end of the inlet duct is formed as a triangular expansion, wherein the hypotenusis of such triangle has a concave shape.
- An immersion tube is provided in the center of the cyclone housing.
- Document EP 0 342 340 A2 is directed to a preheating device having an immersion tube that is arranged eccentrically within the upper part of the cyclone.
- the immersion tube is offset in a direction of a circumferential section which is provided opposite the inlet section.
- Sticky particles are understood to be particles which are characterized by adhesiveness. In general, they have cohesive forces which promote the formation of accretions in processing plants. The actual stickiness can also occur for example due to the mechanical entanglement and cross-linkage of filamentary surface structures.
- the stickiness is also realized by atomic forces such as van der Waals forces or hydrogen bridge bonds.
- the angle of inclination ⁇ extends from 30° to 0°, which results in the fact that the formation of the triangular expansion Q is formed increasingly narrow as seen in gas direction, until it finally no longer is present when reaching the angle of inclination ⁇ of 0°.
- the outer boundary then coincides with the cylindrical outer wall.
- a preferred aspect of the invention consists in that the inlet duct is arranged with an inclination in flow direction towards the particle outlet and the angle of inclination ⁇ is between 10° and 45°.
- a further preferred aspect of the invention consists in that the inner wall of the cyclone has a non-stick coating. Preventing accretions of sticky particles thus is promoted in addition.
- different materials can be used as a non-stick coating. For some applications, the use of polytetrafluoroethylene as a non-stick coating was quite successful.
- the immersion tube is arranged eccentrically in direction of the inlet duct. It is advantageous that it is ensured that upon introduction of the gas streams into the cyclone the majority of sticky particles from the gas streams do not impinge on the immersion tube and partly adhere to the same. Most of the sticky particles thus are advantageously guided past the immersion tube and subjected to the centrifugal forces.
- Subject-matter of the invention finally is the use of the cyclone for separating partly molten particles.
- These partly molten particles for example can be plastic particles, which must be transported in relatively hot gas streams and be separated from the same. These partly molten particles do not stick together in the cyclone, but reach the particle outlet without forming accretions inside the cyclone.
- the cyclone for separating sticky particles from gas streams is shown in three-dimensional form. It includes a cylindrical outer wall 1, an inlet duct 3 and a particle outlet 5. Furthermore, an immersion tube 2 is provided, which is arranged eccentrically in direction of the inlet duct 3. The inlet duct 3 is arranged with an inclination in flow direction towards the particle outlet 5, wherein the angle of inclination ⁇ lies in the range between 10° and 45°.
- Fig. 2 the top view of the cyclone for separating sticky particles from gas streams is shown.
- the immersion tube 2 is arranged eccentrically in direction of the inlet duct 3.
- Fig. 3 the cyclone for separating sticky particles from gas streams is shown with a view to the inlet duct 3.
- the flow cross-section has a triangular expansion Q which laterally is formed by the cylindrical outer wall 1 and by an outer boundary 4.
- the outer angle of inclination ⁇ between the outer boundary 4 and the vertical extends from 30° to 0° (not shown), proceeding from the end of the inlet duct 3 in flow direction of the gas streams. Due to the constructive design of the cyclone, accretions of sticky particles from the gas streams in the interior of the cyclone can be avoided in an advantageous way.
- Fig. 4 the cyclone for separating sticky particles from gas streams is shown according to section A-A in Fig. 2 . Proceeding from 30° (not shown), the angle of inclination ⁇ is formed smaller than is shown in Fig. 3 . The angle of inclination ⁇ here is 25°, so that in this position the triangular expansion Q (not shown) is smaller than in the position shown in Fig. 3 .
- Fig. 5 the cyclone for separating sticky particles from gas streams is shown according to section B-B in Fig. 2 .
- the angle of inclination ⁇ (not shown) is 0°, so that here the cylindrical outer wall 1 coincides with the outer boundary 4.
- the triangular expansion Q (not shown) no longer is formed in this position.
Claims (4)
- Zyklon für die Abscheidung klebriger Partikel aus Gasströmen, bei dem der Strömungsquerschnitt am Ende des Einlasskanals (3) in Richtung zum Partikelaustrag (5) eine dreiecksförmige Erweiterung Q aufweist, die seitlich durch die zylinderförmige Außenwand (1) und durch eine Außenbegrenzung (4) gebildet wird, dadurch gekennzeichnet, dass der äußere Neigungswinkel β zwischen der Außenbegrenzung (4) und der Senkrechten, ausgehend vom Ende des Einlasskanals (3), in Strömungsrichtung der Gasströme von 30° bis 0° verläuft.
- Zyklon nach Anspruch 1, bei dem der Einlasskanal (3) in Strömungsrichtung zum Partikelaustrag (5) geneigt angeordnet ist und der Neigungswinkel α zwischen 10° und 45° beträgt.
- Zyklon nach Anspruch 1 oder 2, bei dem die Innenwand des Zyklons eine Antihaftbeschichtung aufweist.
- Verwendung des Zyklons nach einem der Ansprüche 1 bis 3 zur Abscheidung angeschmolzener Partikel.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200910042013 DE102009042013B4 (de) | 2009-09-21 | 2009-09-21 | Zyklon für die Abscheidung klebriger Partikel aus Gasströmen |
PCT/EP2010/004780 WO2011032620A1 (en) | 2009-09-21 | 2010-08-04 | Cyclone for separating sticky particles from gas streams |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2480335A1 EP2480335A1 (de) | 2012-08-01 |
EP2480335B1 true EP2480335B1 (de) | 2017-12-13 |
Family
ID=43033297
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10744879.7A Active EP2480335B1 (de) | 2009-09-21 | 2010-08-04 | Zyklon zur abscheidung klebriger partikel aus gasströmen |
Country Status (12)
Country | Link |
---|---|
US (1) | US8657934B2 (de) |
EP (1) | EP2480335B1 (de) |
CN (1) | CN102574134A (de) |
AU (1) | AU2010294892B2 (de) |
BR (1) | BR112012006341A2 (de) |
CA (1) | CA2771794C (de) |
DE (1) | DE102009042013B4 (de) |
EA (1) | EA021413B1 (de) |
MA (1) | MA33682B1 (de) |
NO (1) | NO2480335T3 (de) |
TR (1) | TR201802556T4 (de) |
WO (1) | WO2011032620A1 (de) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9211044B2 (en) | 2011-03-04 | 2015-12-15 | Omachron Intellectual Property Inc. | Compact surface cleaning apparatus |
DE102009050165A1 (de) * | 2009-10-21 | 2011-04-28 | Outotec Oyj | Vorrichtung zur Behandlung von Feststoffen und/oder Gasen |
US9642508B1 (en) * | 2012-04-16 | 2017-05-09 | Billy Goat Indutries, Inc. | Debris-collecting apparatus and method of collecting debris |
US9820621B2 (en) | 2013-02-28 | 2017-11-21 | Omachron Intellectual Property Inc. | Surface cleaning apparatus |
US9238235B2 (en) | 2013-02-28 | 2016-01-19 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9227151B2 (en) | 2013-02-28 | 2016-01-05 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9227201B2 (en) | 2013-02-28 | 2016-01-05 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9295995B2 (en) | 2013-02-28 | 2016-03-29 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
CN104437906B (zh) * | 2013-09-13 | 2017-05-31 | 中国石油化工股份有限公司 | 一种旋风分离器的自动出料装置及其控制方法 |
WO2016007730A1 (en) * | 2014-07-09 | 2016-01-14 | Sudhin Biopharma | Particle settling devices |
US10596492B2 (en) | 2014-07-09 | 2020-03-24 | Sudhin Biopharma | Particle settling devices |
WO2016139838A1 (ja) * | 2015-03-05 | 2016-09-09 | ブラザー工業株式会社 | 燃料電池システムにおける気液分離器 |
SE538760C2 (sv) * | 2015-03-12 | 2016-11-15 | Valmet Oy | Cyclone separator arrangement and method |
US20180036653A1 (en) * | 2016-08-03 | 2018-02-08 | Jci Cyclonic Technologies Ltd. | Dual cyclone separator |
JP6597744B2 (ja) * | 2017-09-29 | 2019-10-30 | ダイキン工業株式会社 | 油分離器 |
CN107812621A (zh) * | 2017-11-20 | 2018-03-20 | 江苏太湖锅炉股份有限公司 | 旋风分离除尘器 |
BR112020021267A2 (pt) | 2018-04-18 | 2021-01-26 | Sudhin Biopharma | dispositivos de sedimentação de partículas |
USD916403S1 (en) * | 2018-06-12 | 2021-04-13 | Nantong Taimei Environmental Protection Technology | Dust collector |
USD916404S1 (en) * | 2018-06-12 | 2021-04-13 | Nantong Taimei Environmental Protection Technology | Dust collector |
WO2020046603A1 (en) * | 2018-08-27 | 2020-03-05 | Sierra Nevada Corporation | Low-gravity water capture device with water stabilization |
USD920611S1 (en) * | 2018-12-18 | 2021-05-25 | Bissell Inc. | Vacuum cleaner foot, wand, and handle |
USD914306S1 (en) * | 2018-12-18 | 2021-03-23 | Bissell Inc. | Vacuum cleaner foot, wand, and handle |
USD914308S1 (en) * | 2019-08-09 | 2021-03-23 | Oneida Air Systems, Inc. | Upright cylindrical pre-separator for dust collector |
CA3172276A1 (en) | 2020-03-19 | 2021-09-23 | Dhinakar S. Kompala | Particle settling devices |
USD917807S1 (en) * | 2020-04-17 | 2021-04-27 | Li Tian | Cyclone dust collector |
US11850605B2 (en) * | 2022-03-01 | 2023-12-26 | Saudi Arabian Oil Company | Apparatus and method to separate and condition multiphase flow |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2349027A1 (de) * | 1973-09-27 | 1975-04-03 | Leisegang Umwelttechnik Kg | Zentrifugalabscheider |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3513642A (en) * | 1968-07-25 | 1970-05-26 | Milan S Cornett | Centrifugal dust separator |
US3745752A (en) * | 1970-12-30 | 1973-07-17 | Envirotech Corp | Fluid inlet structure for cyclone collectors |
JPS57117360A (en) | 1981-01-12 | 1982-07-21 | Mitsubishi Mining & Cement Co Ltd | Cyclone |
AU1397783A (en) * | 1982-05-12 | 1983-11-17 | Krw Energy Systems Inc. | Cyclone with porous inner wall |
JPS6168152A (ja) * | 1984-09-10 | 1986-04-08 | Nippon Donarudoson Kk | サイクロン分離器 |
GB2202468A (en) * | 1987-03-25 | 1988-09-28 | Smidth & Co As F L | Cyclone |
DE3817355A1 (de) * | 1988-05-20 | 1989-11-30 | Krupp Polysius Ag | Schwebegas-waermetauscher |
DE8807793U1 (de) * | 1988-06-15 | 1988-12-15 | Dozent Doppelzyklon-Entstaubungsanlagen Gmbh, 4300 Essen, De | |
DE8811275U1 (de) * | 1988-09-07 | 1988-10-27 | Apparatebau Rothemuehle Brandt + Kritzler Gmbh, 5963 Wenden, De | |
DE19858675A1 (de) * | 1998-07-27 | 2000-02-24 | Patentstelle Fuer Die Deutsche | Verfahren zum Abscheiden von gasförmigen Alkaliverbindungen und/oder flüssigen, aufgeschmolzenen oder klebrigen Feststoffteilchen aus heißen Gasströmen |
EP1308213A1 (de) * | 2001-10-30 | 2003-05-07 | Alstom (Switzerland) Ltd | Zentrifugalabschneider, insbesondere für einen Reaktor mit zirkulierendem Wirbelbett |
US6926749B1 (en) * | 2003-06-27 | 2005-08-09 | Fisher-Klosterman | Cyclone separator with compact inlet |
CN100490984C (zh) | 2005-04-15 | 2009-05-27 | 清华大学 | 一种旋风分离装置 |
CN2936439Y (zh) | 2006-04-26 | 2007-08-22 | 哈尔滨锅炉厂有限责任公司 | 偏心式高效旋风分离器 |
-
2009
- 2009-09-21 DE DE200910042013 patent/DE102009042013B4/de not_active Expired - Fee Related
-
2010
- 2010-08-04 CN CN2010800422041A patent/CN102574134A/zh active Pending
- 2010-08-04 EP EP10744879.7A patent/EP2480335B1/de active Active
- 2010-08-04 US US13/497,120 patent/US8657934B2/en not_active Expired - Fee Related
- 2010-08-04 BR BR112012006341A patent/BR112012006341A2/pt not_active IP Right Cessation
- 2010-08-04 EA EA201290126A patent/EA021413B1/ru not_active IP Right Cessation
- 2010-08-04 AU AU2010294892A patent/AU2010294892B2/en not_active Ceased
- 2010-08-04 WO PCT/EP2010/004780 patent/WO2011032620A1/en active Application Filing
- 2010-08-04 NO NO10744879A patent/NO2480335T3/no unknown
- 2010-08-04 TR TR2018/02556T patent/TR201802556T4/tr unknown
- 2010-08-04 CA CA2771794A patent/CA2771794C/en not_active Expired - Fee Related
-
2012
- 2012-04-19 MA MA34789A patent/MA33682B1/fr unknown
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2349027A1 (de) * | 1973-09-27 | 1975-04-03 | Leisegang Umwelttechnik Kg | Zentrifugalabscheider |
Also Published As
Publication number | Publication date |
---|---|
EA201290126A1 (ru) | 2012-10-30 |
DE102009042013B4 (de) | 2015-05-07 |
US8657934B2 (en) | 2014-02-25 |
US20120180662A1 (en) | 2012-07-19 |
NO2480335T3 (de) | 2018-05-12 |
DE102009042013A1 (de) | 2011-03-24 |
AU2010294892A1 (en) | 2012-04-26 |
WO2011032620A1 (en) | 2011-03-24 |
AU2010294892B2 (en) | 2014-11-06 |
TR201802556T4 (tr) | 2018-03-21 |
EP2480335A1 (de) | 2012-08-01 |
EA021413B1 (ru) | 2015-06-30 |
CA2771794A1 (en) | 2011-03-24 |
CN102574134A (zh) | 2012-07-11 |
BR112012006341A2 (pt) | 2016-03-29 |
MA33682B1 (fr) | 2012-10-01 |
CA2771794C (en) | 2016-01-05 |
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